Cell-based production of nanulosonates

ABSTRACT

The present invention relates to the cell-based production of bacterial nonulosonates and their biosynthetic precursors. Specifically, the present invention provides recombinant cells for the production of pseudaminic acid, legionaminic acid, UDP-2,4-diacetamido-2,4,6-trideoxy-β-L-altropyranose, and UDP-2,4-diacetamido-2,4,6-trideoxy-α-D-glucopyranose. Methods for producing the sugars are also provided.

FIELD OF THE INVENTION

The present invention relates to the cell-based production of bacterial nonulosonates. More specifically, the present invention relates to the cell-based production of bacterial nonulosonates and their biosynthetic precursors.

BACKGROUND OF THE INVENTION

Nonulosonic sugars are a family of nine-carbon α-keto acids that are predominantly found on the outer surfaces of both eukaryotic and bacterial cells. Sialic acid (see FIG. 1), which is the best characterized member of this family, plays a crucial role in animal physiology; for this reason, sialic acid and its derivatives have been extensively used as drug targeting molecules (Javant et al, 2007), anti-viral drugs (von Itzstein, 2007), cell-imaging agents (Mahal et al, 1997; Hsu et al, 2007), and as supplements in nutraceuticals (Colombo et al, 2003; Wang et al, 2007).

Two other structurally distinct nonulosonic sugars, pseudaminic (Schoenhofen et al, 2006a) (Pse) and legionaminic (Schoenhofen et al, 2009) (Leg) acid (FIG. 1), and their biosynthetic pathways have also been characterized. These sialic acid-like sugars are constituents of microbial glycans, which are associated with important virulence factors, including flagella (McNally et al, 2007), capsules (Kiss et al, 2001), and lipopolysacchrides (Knirel et al, 2003 (LPS). Many commensal, as well as pathogenic bacteria, notably Campylobacter jejuni, Campylobacter coli, Clostridium botulinum, Escherichia coli O161, Helicobacter pylori, Legionella pneumophila, Vibrio parahaemolyticus and Pseudomonas aeruginosa, biosynthesize and decorate their surfaces with these nonulosonic acids, whose function(s) remains unclear.

The structural similarities and evolutionary history (Lewis et al, 2009) shared between these three nonulosonic sugars has raised considerable interest in understanding the mammalian sialobiology associated with bacterial-derived Pse and Leg. The biosynthesis of Pse and Leg parallels that of sialic acid and involves the condensation of a 6-carbon amino sugar intermediate with phosphoenolpyruvate (PEP) to generate the corresponding nonulosonate. In contrast to sialic acid biosynthesis in bacteria, which involves condensation of N-acetylmannosamine (ManNAc) with PEP, both Pse and Leg utilize unusual 2,4-diacetamido-2,4,6-trideoxy hexoses (DATDH) for the synthase step.

Pse is biosynthesized from UDP-N-acetylglucosamine (UDP-GlcNAc) in a five-step enzymatic transformation (Schoenhofen et al, 2006a) (see Table 1 and FIG. 2). A dedicated dehydratase (PseB) and aminotransferase (PseC) pair (Schoenhofen et al, 2006b), converts UDP-GlcNAc into UDP-4-amino-4,6-dideoxy-β-L-AltNAc. An acetyltransferase, PseH, and a UDP-sugar hydrolase, PseG, transform this UDP-activated sugar intermediate into 2,4-diacetamido-2,4,6-trideoxy-L-altropyranose (6-deoxy-AltdiNAc). The Pse synthase, PseI, performs the PEP-dependent condensation with 6-deoxy-AltdiNAc to liberate 5,7-diacetamido-3,5,7,9-tetradeoxy-L-glycero-L-manno-nonulosonic acid or pseudaminic acid.

TABLE 1 The enzymes involved in UDP-6-deoxy-AltdiNAc, pseudaminic acid (Pse), UDP-BacdiNAc and legionaminic acid (Leg) biosynthesis. Enzymes are shown in sequential order, where each product is a substrate for the next biosynthetic step. The initial substrate for each pathway is UDP-GlcNAc. Enzyme In vitro Enzyme Nomenclature function Biosynthetic product(s) UDP-6-deoxy-AltdiNAc and Pseudaminic acid route PseB UDP-GlcNAc 4,6- UDP-2-acetamido-2,6-dideoxy-β-L-arabino-hexos- dehydratase and 5- 4-ulose epimerase PseC aminotransferase UDP-4-amino-4,6-dideoxy-β-L-AltNAc or UDP-2-acetamido-4-amino-2,4,6-trideoxy-β-L-Alt PseH N-acetyltransferase UDP-2,4-diacetamido-2,4,6-trideoxy-β-L-Alt (UDP-6-deoxy-AltdiNAc) PseG UDP-sugar hydrolase 2,4-diacetamido-2,4,6-trideoxy-L-Alt (6-deoxy-AltdiNAc) PseI Pse synthase 5,7-diacetamido-3,5,7,9-tetradeoxy-L-glycero-L- manno-nonulosonic acid (Pse) UDP-BacdiNAc and Legionaminic acid route PglF UDP-GlcNAc 4,6- UDP-2-acetamido-2,6-dideoxy-α-D-xylo-hexos-4- dehydratase ulose PglE aminotransferase UDP-4-amino-4,6-dideoxy-α-D-GlcNAc or UDP-2-acetamido-4-amino-2,4,6-trideoxy-α-D-Glc PglD N-acetyltransferase UDP-2,4-diacetamido-2,4,6-trideoxy-α-D-Glc (UDP-BacdiNAc) LegG UDP-sugar hydrolase 2,4-diacetamido-2,4,6-trideoxy-D-Man and 2-epimerase (6-deoxy-MandiNAc) LegI Leg synthase 5,7-diacetamido-3,5,7,9-tetradeoxy-D-glycero-D- galacto-nonulosonic acid (Leg)

Leg may also be biosynthesized from UDP-N-acetylglucosamine (UDP-GlcNAc) in a five-step enzymatic transformation (Schoenhofen et al, 2009; Schoenhofen et al, 2006b; Oliver et al, 2006; Glaze et al, 2008; see Table 1 and FIG. 2). Dehydratase PglF and aminotransferase PglE pair (Schoenhofen et al, 2006b) convert UDP-GlcNAc into UDP-4-amino-4,6-dideoxy-α-D-GlcNAc. Acetyltransferase PglD and hydrolyzing 2-epimerase LegG transform this UDP-activated sugar intermediate into 2,4-diacetamido-2,4,6-trideoxy-D-mannopyranose (6-deoxy-MandiNAc). The Leg synthase, LegI, performs the PEP-dependent condensation with 6-deoxy-MandiNAc to liberate 5,7-diacetamido-3,5,7,9-tetradeoxy-D-glycero-D-galacto-nonulosonic acid (legionaminic acid). Enzymes functionally similar to PglF, PglE and PglD also exist, for example the C. jejuni LegB, LegC and LegH (respectively) enzymes, which produce identical sugar products except that they are GDP-linked biosynthetic intermediates (Schoenhofen et al, 2009). Here, PglFED produce UDP-BacdiNAc starting from UDP-GlcNAc (see Table 1). Similarly, certain LegG enzymes, as in C. jejuni, may utilize a GDP-linked substrate

The bacterial nonulosonic acids are a medically and biotechnologically important family of cell-surface carbohydrates. Current methods for producing these complex sugars allows the isolation of only limited, sub-gram quantities from natural resources, or via currently available chemical or enzymatic synthesis in vitro. Additionally, the cost of enzyme preparation, reagents and cofactors required for in vitro synthesis is quite significant.

There remains a need in the art for a method that can generate significant quantities of Pse and Leg in a cost-effective manner.

SUMMARY OF THE INVENTION

The present invention relates to the cell-based production of bacterial nonulosonates. More specifically, the present invention relates to the cell-based production of bacterial nonulosonates and their biosynthetic precursors.

The present invention provides a recombinant cell for the production of pseudaminic acid, comprising an inactivated GlcNAc-6-P deacetylase gene, a gene encoding PseB enzyme function, a gene encoding PseC enzyme function, a gene encoding PseH enzyme function, a gene encoding PseI enzyme function, a gene encoding PseG enzyme function, a gene encoding a GlcNAc-6-P mutase, and a gene encoding a GlcNAc-1-P uridyltransferase.

In the recombinant cell just described, the PseB, PseC, PseH, and PseI enzyme functions may be genes from H. pylori, the PseG enzyme function may be a gene from C. jejuni, and the GlcNAc-6-P mutase and GlcNAc-1-P uridyltransferase genes may be from S. cerevisiae. Optionally, the recombinant cell may further comprise an inactivated sialic acid transporter gene, an inactivated sialic acid aldolase gene, or a combination thereof; the sialic acid transporter gene may be nanT, and the sialic acid aldolase gene may be nanA.

In the recombinant cell described above, the cell may be an E. coli cell.

In one example, in the recombinant cell for the production of pseudaminic acid, the recombinant cell may be an E. coli cell, the sialic acid transporter gene may be nanT, the sialic acid aldolase gene may be nanA, the GlcNAc-6-P deacetylase gene may be nagA, the PseB gene may encode SEQ ID NO:1, the PseC gene may encode SEQ ID NO:2, the PseH gene may encode SEQ ID NO:3, the PseI gene may encode SEQ ID NO:4, the PseG gene may encode SEQ ID NO:5, the gene encoding GlcNAc-6-P mutase may be agm1, and the gene encoding GlcNAc-1-P uridyltransferase may be uap1.

In the recombinant cell described above, the growth medium for the recombinant cell may be supplemented with palmitate; alternatively, the recombinant cell may further comprising a gene encoding acetyl-CoA synthase.

One specific example of the recombinant cell for the production of pseudaminic acid as described above is that of IDAC deposit No. 060411-02.

The present invention also provides a recombinant cell for the production of legionaminic acid, comprising an inactivated GlcNAc-6-P deacetylase gene, a gene encoding PglF enzyme function, a gene encoding PglE enzyme function, a gene encoding PglD enzyme function, a gene encoding LegI enzyme function, a gene encoding LegG enzyme function, a gene encoding a GlcNAc-6-P mutase, and a gene encoding a GlcNAc-1-P uridyltransferase.

In the recombinant cell just described, the PglF, PglE, and PglD enzyme functions may be genes from C. jejuni, the LegI enzyme function may be genes from C. jejuni or L. pneumophila, the LegG enzyme function may be a gene from L. pneumophila LegG, and the GlcNAc-6-P mutase and GlcNAc-1-P uridyltransferase genes may be from S. cerevisiae. Optionally, the recombinant cell may further comprise an inactivated sialic acid transporter gene, an inactivated sialic acid aldolase gene, or a combination thereof; the sialic acid transporter gene may be nanT, and the sialic acid aldolase gene may be nanA. In the recombinant cell described above, the cell may be an E. coli cell.

In one example, in the recombinant cell for the production of legionaminic acid, the recombinant cell may be an E. coli cell, the sialic acid transporter gene may be nanT, the sialic acid aldolase gene may be nanA, the GlcNAc-6-P deacetylase gene may be nagA, the PglF gene may encode SEQ ID NO:6, the PglE gene may encode SEQ ID NO:7, the PglD gene may encode SEQ ID NO:8, the LegI gene may encode SEQ ID NO:9 or SEQ ID NO:10, the LegG gene may encode SEQ ID NO:11, the GlcNAc-6-P mutase gene may be agm1, and the GlcNAc-1-P uridyltransferase gene may be uap1.

The recombinant cell for the production of legionaminic acid as described above may further comprise an inactivated ManNAc-6-P epimerase gene, an inactivated undecaprenyl-P/UDP-GlcNAc transferase gene, or a combination thereof. The ManNAc-6-P epimerase gene may be nanE, and the undecaprenyl-P/UDP-GlcNAc transferase gene may be wecA.

Additionally, in the recombinant cell for the production of legionaminic acid described above, the growth medium for the recombinant cell may be supplemented with palmitate; alternatively, the recombinant cell may further comprising a gene encoding acetyl-CoA

The present invention provides a method for the production of pseudaminic acid (5,7-diacetamido-3,5,7,9-tetradeoxy-L-glycero-L-manno-nonulosonic acid), comprising growing the recombinant cell for the production of pseudaminic acid as described above and recovering the produced pseudaminic acid.

Similarly, the present invention provides a method for the production of legionaminic acid (5,7-diacetamido-3,5,7,9-tetradeoxy-D-glycero-D-galacto-nonulosonic acid), comprising growing the recombinant cell for the production of legionaminic acid as described above and recovering the produced legionaminic acid.

The present invention further provides a recombinant cell for the production of UDP-2,4-diacetamido-2,4,6-trideoxy-β-L-altropyranose (UDP-6-deoxy-AltdiNAc), comprising an inactivated GlcNAc-6-P deacetylase gene, a gene encoding PseB enzyme function, a gene encoding PseC enzyme function, a gene encoding PseH enzyme function, a gene encoding GlcNAc-6-P mutase, and a gene encoding a GlcNAc-1-P uridyltransferase.

In the recombinant cell as just described, the PseB, PseC, and PseH enzyme functions may be from H. pylori, and the GlcNAc-6-P mutase and GlcNAc-1-P uridyltransferase genes may be from S. cerevisiae. Optionally, the recombinant cell may further comprise an inactivated sialic acid transporter gene, an inactivated sialic acid aldolase gene, or a combination thereof; the sialic acid transporter gene may be nanT, and the sialic acid aldolase gene may be nanA. The recombinant cell as described above may be an E. coli cell.

In one example of a recombinant cell for the production of UDP-6-deoxy-AltdiNAc, the recombinant cell may be an E. coli cell, the sialic acid transporter gene may be nanT, the sialic acid aldolase gene may be nanA, the GlcNAc-6-P deacetylase gene may be nagA, the PseB gene may encode SEQ ID NO:1, the PseC gene may encode SEQ ID NO:2, the PseH gene may encode SEQ ID NO:3, the GlcNAc-6-P mutase gene may be agm1, and the GlcNAc-1-P uridyltransferase gene may be uap1.

The present invention also provides a method for the production of UDP-2,4-diacetamido-2,4,6-trideoxy-β-L-altropyranose (UDP-6-deoxy-AltdiNAc), comprising growing the recombinant cell for the production of UDP-6-deoxy-AltdiNAc as described above and recovering the produced UDP-2,4-diacetamido-2,4,6-trideoxy-β-L-altropyranose.

The present invention additionally provides a recombinant cell for the production of UDP-2,4-diacetamido-2,4,6-trideoxy-α-D-glucopyranose (UDP-BacdiNAc), comprising an inactivated GlcNAc-6-P deacetylase gene, a gene encoding PglF enzyme function, a gene encoding PglE enzyme function, and a gene encoding PglD enzyme function, a gene encoding GlcNAc-6-P mutase, and a gene encoding a GlcNAc-1-P uridyltransferase.

In the recombinant cell as just described, the PglF, PglE, and PglD genes may be from C. jejuni, and the GlcNAc-6-P mutase and GlcNAc-1-P uridyltransferase genes may be from S. cerevisiae. Optionally, the recombinant cell may further comprise an inactivated sialic acid transporter gene, an inactivated sialic acid aldolase gene, or a combination thereof; the sialic acid transporter gene may be nanT, and the sialic acid aldolase gene may be nanA.

The recombinant cell for production of UDP-BacdiNAc described above may further comprising an inactivated undecaprenyl-P/UDP-GlcNAc transferase gene. The undecaprenyl-P/UDP-GlcNAc transferase gene may be wecA.

The recombinant cell for production of UDP-BacdiNAc described above may be an E. coli cell.

In one example of a recombinant cell for production of UDP-BacdiNAc, the recombinant cell may be an E. coli cell, the sialic acid transporter gene may be nanT, the sialic acid aldolase gene may be nanA, the GlcNAc-6-P deacetylase gene may be nagA, the PglF gene may encode SEQ ID NO:6, the PglE gene may encode SEQ ID NO:7, the PglD gene may encode SEQ ID NO:8, the GlcNAc-6-P mutase gene may be agm1, and the GlcNAc-1-P uridyltransferase gene may be uap1.

One specific example of the recombinant cell for the production of UDP-BacdiNAc as described above is that of IDAC deposit No. 060411-01.

The present invention also provides a method for the production of UDP-2,4-diacetamido-2,4,6-trideoxy-α-D-glucopyranose (UDP-BacdiNAc), comprising growing the recombinant cell for the production of UDP-BacdiNAc as described above and recovering the produced UDP-2,4-diacetamido-2,4,6-trideoxy-α-D-glucopyranose.

Additional aspects and advantages of the present invention will be apparent in view of the following description. The detailed description and examples, while indicating preferred embodiments of the invention, are given by way of illustration only, as various changes and modifications within the scope of the invention will become apparent to those skilled in the art in light of the teachings of this invention.

BRIEF DESCRIPTION OF THE DRAWINGS

These and other features of the invention will now be described by way of example, with reference to the appended drawings, wherein:

FIG. 1 shows the structures of sialic acid and sialic acid-like sugars. Sialic acid (Neu5Ac; D-glycero-D-galacto configuration), pseudaminic acid (Pse5Ac7Ac; L-glycero-L-manno configuration), legionaminic acid (Leg5Ac7Ac; D-glycero-D-galacto configuration), 4-epi-legionaminic acid (4eLeg5Ac7Ac; D-glycero-D-talo configuration), and 8-epi-legionaminic acid (8eLeg5Ac7Ac; L-glycero-D-galacto configuration) are shown. For reference, the 9 carbon atoms of sialic acid are numbered, and the functional groups that are different than those present on sialic acid-like sugars are circled. Moreover, stereochemical differences of bacterial sialic acid-like sugars to that of sialic acid are indicated by numbering of the respective carbon centers.

FIG. 2 shows the production pathway for pseudaminic acid, legionaminic acid, and UDP-activated 2,4-diacetamido-2,4,6-trideoxy hexoses (DATDH), specifically UDP-6-deoxy-AltdiNAc or UDP-BacdiNAc, by metabolically engineered E. coli. The non-native, yeast-derived enzymes, Agm1 and Uap1, were used to activate exogenously fed GlcNAc into UDP-GlcNAc. This substrate then entered either pseudaminic acid or legionaminic acid biosynthesis via PseBCHGI or PglFED/LegGI, respectively. Important for production was removal of the 2-acetamido deacetylase, NagA, which prevented the degradation of GlcNAc-6-P and possible degradation of 6-deoxy-AltdiNAc. Abbreviations: Agm1: N-acetylglucosamine mutase, Uap1: N-acetyl-glucosamine-1-P uridyltransferase, PseB/PglF: dehydratase, PseC/PglE: aminotransferase, PseH/PglD: acetyltransferase, PseG: UDP-sugar hydrolase, PseI: Pse synthase, LegG: UDP-sugar hydrolase and 2-epimerase, LegI: Leg synthase, NagA: GlcNAc-6-P deacetylase, NagE/ManXYZ; GlcNAc- and ManNAc-specific PTS transporters. See Table 1 for the PseBCHGI and PglFED/LegGI sugar products.

FIG. 3 shows a LCMS ESI⁺ spectrum of pseudaminic acid produced from E. coli BRL02 expressing the pseBCHGI and agm1/uap1 genes (BRL02 pBRL179) when grown on glycerol/GlcNAc. Exogenously fed GlcNAc was converted to UDP-GlcNAc by Agm1/Uap1, and the PseBCHGI pathway converted UDP-GlcNAc into pseudaminic acid as detected by LCMS ESI. Peaks at m/z of 317.5 (M−OH) and 335.4 (M+H) were observed, where M is the characteristic mass of pseudaminic acid.

FIG. 4 shows LCMS ESI⁺ analysis of cell-free culture broth from BRL04/pseBCHGI/agm1/uap1 cells (BRL04/pBRL175/pBRL178) in a glycerol/GlcNAc-batch fermentation. FIG. 4A showed a clear ion-extraction peak for pseudaminic acid with m/z values of 317(M−OH), 335 (M+H) and 357 (M+Na). These ion extraction peaks were not present in the negative control production culture (data not shown). To confirm that these m/z values are derived from authentic pseudaminic acid, cell-free broth from the negative control culture was spiked with a pseudaminic acid standard. As shown, the ion-extraction peak of the spiked sample (FIG. 4B) was identical to the pseudaminic acid produced from the BRL04/pseBCHGI/agm1/uap1 (BRL04/pBRL175/pBRL178) fermentation (FIG. 4A).

FIG. 5 shows an LCMS ESI⁺ spectrum demonstrating the effect of increasing intracellular acetyl-CoA levels on pseudaminic acid production. Acetyl-CoA synthesis was up-regulated through β-oxidation of palmitate, which was supplemented into the production culture at a total of 0.6 mg L⁻¹. The LCMS ESI⁺ analysis of cell-free culture broth from BRL04/pBRL175/pBRL178 cells (as described for FIG. 4) with the fermentation supplemented with palmitate, clearly shows an ion-extraction peak for pseudaminic acid with m/z values of 317(M-OH), 335 (M+H) and 357 (M+Na).

FIG. 6 shows LCMS ESI⁺ spectrum of pseudaminic acid in water, to validate the detection process (i.e. standard or positive control). Pseudaminic acid was separated by a Hypercarb HPLC column using an isocratic elution with water. Peaks at m/z of 317.4 (M−OH), 335.4 (M+H) and 357.5 (M+Na) were observed with a detection limit of 40 mg L⁻¹ of pseudaminic acid, where M is the characteristic mass of pseudaminic acid.

FIG. 7 shows the structure of UDP-2,4-diacetamido-2,4,6-trideoxy-β-L-altropyranose (UDP-6-deoxy-AltdiNAc) and UDP-2,4-diacetamido-2,4,6-trideoxy-α-D-glucopyranose (UDP-BacdiNAc), precursors for production of pseudaminic acid and legionaminic acid, respectively.

FIG. 8 shows a CE-MS spectra (negative ion mode) of non-native UDP-activated 2,4-diacetamido-2,4,6-trideoxy hexoses (m/z 630.9) biosynthesized by E. coli. The enzymes involved in the biosynthesis of UDP-DATDH precursors from either the pseudaminic acid (PseBCH) or legionaminic acid (PglFED) pathway were expressed in the ΔnagA BRL04/agm1/uap1 strain. Lysates from the production cultures were analyzed by CE-MS in the negative-ion mode, and m/z peaks of 630.9 were observed from both UDP-6-deoxy-AltdiNAc (UDP-2,4-diacetamido-2,4,6-trideoxy-β-L-altropyranose; FIG. 8A) (PseBCH) and UDP-BacdiNAc (UDP-2,4-diacetamido-2,4,6-trideoxy-α-D-glucopyranose; FIG. 8B) (PglFED) samples. The negative control is shown in FIG. 8C, indicating an absence of m/z peak 630.9, as expected. The strain BRL04/pBRL151/pBRL178 was used for UDP-2,4-diacetamido-2,4,6-trideoxy-β-L-altropyranose (UDP-6-deoxy-AltdiNAc) production and strain BRL04/pBRL152/pBRL178 was used for UDP-2,4-diacetamido-2,4,6-trideoxy-α-D-glucopyranose (UDP-BacdiNAc) production.

FIG. 9 shows exopolysaccharides that were deleted in E. coli K-12 for the production of pseudaminic acid, including i) enterobacterial common antigen (ECA), ii) colanic acid and iii) poly-N-acetylglucosamine. The 4-acetamido-6-deoxy sugar, fucosamine, is a constituent of ECA and colanic acid. Each gene cluster was removed using lambda Red-mediated recombination. Abbreviations, FucN4Ac: 4-acetamido-4,6-dideoxy-D-galactose, ManNAcA: N-acetyl-D-mannosaminuronic acid, Gal: galactose, Pyr: pyruvate

FIG. 10 shows the production of legionaminic acid from engineered E. coli. Legionaminic acid is biosynthesized from UDP-2,4-diacetamido-2,4,6-trideoxy-α-D-glucopyranose (UDP-BacdiNAc, labelled here as UDP-Bac) via a hydrolyzing 2-epimerase, LegG (or NeuC homolog), and a Leg synthase, LegI (or NeuB homolog). The epimerization at C2 by LegG generates a 2-acetamido-6-deoxy mannose intermediate (6-deoxy-MandiNAc) that is not likely accepted by the NagA/NagB catabolic pathway, but instead has to undergo a second epimerization at C2 via NanE to generate a degradable sugar adduct.

DETAILED DESCRIPTION OF THE INVENTION

The present invention relates to the cell-based production of bacterial nonulosonates. More specifically, the present invention relates to the cell-based production of bacterial nonulosonates and their biosynthetic precursors.

The present invention provides a recombinant cell for the production of pseudaminic acid, comprising an inactivated sialic acid transporter gene, an inactivated sialic acid aldolase gene, an inactivated GlcNAc-6-P deacetylase gene, a gene encoding PseB enzyme function, a gene encoding PseC enzyme function, a gene encoding PseH enzyme function, a gene encoding PseI enzyme function, a gene encoding PseG enzyme function, a gene encoding a GlcNAc-6-P mutase, and a gene encoding a GlcNAc-1-P uridyltransferase.

The present invention also provides a recombinant cell for the production of legionaminic acid, comprising an inactivated sialic acid transporter gene, an inactivated sialic acid aldolase gene, an inactivated GlcNAc-6-P deacetylase gene, a gene encoding PglF enzyme function, a gene encoding PglE enzyme function, a gene encoding PglD enzyme function, a gene encoding LegI enzyme function, a gene encoding LegG enzyme function, a gene encoding a GlcNAc-6-P mutase, and a gene encoding a GlcNAc-1-P uridyltransferase.

By the term “recombinant cell”, also referred to herein as “recombinant strain”, it is meant any suitable recombinant cell engineered to comprise the appropriate enzymes as listed above. As will be appreciated by one of skill in the art, this may be done using standard molecular biology techniques that are well-known in the art. The recombinant cell may be any suitable microorganism, such as a prokaryotic or eukaryotic cell. For example, the recombinant cell may be a bacterial or yeast cell; the recombinant bacterial or yeast cell may also be a bacterial or yeast strain that has UDP-GlcNAc-utilizing pathways but that does not normally produce the above-listed end products. Alternatively, the recombinant cell may be part of any suitable recombinant expression system, such as mammalian cell lines or insect cell lines (Higgins, 2010; Sethuraman & Stadheim, 2006; Chiba & Jigami, 2007). Without wishing to be limiting in any manner, the recombinant cell may be selected from the group consisting of Escherichia coli, Saccharomyces cerevisiae, Pichia pastoris, Hansenula polymorpha, Kluyveromyces lactis, Candida albicans, Chinese hamster ovary (CHO) cell lines, or murine myeloma cell lines. The recombinant cell does not include naturally-occurring cells that produce pseudaminic or legionamic acid (such as Escherichia coli O161), but does include naturally-occurring cells in which the production of pseudaminic or legionamic acid has been increased, improved, or enhanced by engineering to comprise the enzymes listed herein. In a specific, non-limiting example, the recombinant cell may be an Escherichia coli cell.

The recombinant cells described herein may be part of a cell-based system for producing the legionaminic acid, pseudaminic acid, or respective biosynthetic precursors. By the term “cell-based system”, it is meant that the recombinant strains described herein are one component and others may be included. Components of the system may include, but are not limited to the recombinant cells described herein, culture medium (also referred to herein as “growth medium”), and supplements. The culture medium may be any suitable culture medium; as would be known to those skilled in the biochemical arts, the choice of culture medium may be based on the type of recombinant cell. Without wishing to be limiting in any manner, supplements to the culture medium may include palmitate. In an alternative to supplementation with palmitate, the recombinant cell may further comprise overexpression of a gene encoding acetyl-CoA synthetase, where the enzyme joins acetate and coenzymeA (CoA) to form acetyl-CoA (Lin et al., 2006).

Pseudaminic acid, also referred to herein as “Pse”, “Pse5Ac7Ac”, or “5,7-diacetamido-3,5,7,9-tetradeoxy-L-glycero-L-manno-nonulosonic acid”, is a nine-carbon α-keto acid. Its structure is shown in FIG. 1. The recombinant cell used for production of Pse comprises genes encoding PseB, PseC, PseH, PseG, and PseI enzyme function. By the term “encoding Pse[ ] enzyme function”, also referred to herein as “Pse genes”, it is meant that the genes encode an enzyme with a function equivalent to that of Pse[ ]; these enzyme notations and their functions are described in Table 1 and FIG. 2. The Pse genes inserted into the recombinant cell may be from any suitable source, including any biological source capable of producing pseudaminic acid; for example, and without wishing to be limiting in any manner, these genes may be from Aeromonas punctata, A. hydrophila, P. aeruginosa, Sinorhizobium meliloti, Rhizobium sp. NGR234, H. pylori, C. jejuni, C. coli, or any other suitable source. The recombinant cell for production of Pse also comprises genes encoding GlcNAc-6-P mutase and GlcNAc-1-P uridyltransferase (Table 2 and FIG. 2). The GlcNAc-6-P mutase and GlcNAc-1-P uridyltransferase genes may be from any suitable source; as would be known to those of skill in the art, many biological sources comprise GlcNAc-6-P mutase or GlcNAc-1-P uridyltransferase genes, and any of these may be used in the present invention. For example, and without wishing to be limiting in any manner, the genes may be from S. cerevisiae, Candida albicans, Homo sapiens, Drosophila melanogaster, or any other suitable source.

Additionally, the recombinant cell used for production of Pse comprises inactivated GlcNAc-6-P deacetylase gene, described in Table 2. Optionally, the recombinant cell used for production of Pse may further comprise an inactivated sialic acid transporter gene, and/or an inactivated sialic acid aldolase gene. As would be understood by those of skill in the art, the source of the inactivated genes will be dependent on the type of recombinant cell used. By the term “inactivated”, it is meant that the gene does not encode a functional product. The gene may be rendered inactive by any suitable method known in the art, for example, but not limited to partial or complete deletion of the gene DNA, or insertion of additional DNA within the gene (resulting in the inability to produce a functional gene product or enzyme).

TABLE 2 Genes manipulated in recombinant cells (E. coli) for the production of pseudaminic acid, legionaminic acid, or respective biosynthetic precursors (in addition to those of Table 1). Gene Description Catalytic Activity or Function of Protein Deletions or Inactivations sialic acid Transport of sialic acid across biological membranes transporter sialic acid Sialic acid (Neu5Ac) → N-acetyl-D-mannosamine aldolase (ManNAc) + pyruvate GlcNAc-6-P N-acetyl-D-glucosamine 6-phosphate → D- deacetylase glucosamine 6-phosphate + acetate Additions GlcNAc-6-P Interconverts N-acetyl-D-glucosamine 6-phosphate and mutase N-acetyl-α-D-glucosamine 1-phosphate GlcNAc-1-P UTP + N-acetyl-α-D-glucosamine 1-phosphate → uridyltransferase pyrophosphate + UDP-N-acetyl-α-D-glucosamine (UDP-GlcNAc)

In one specific, non-limiting example, the recombinant cell for production of pseudaminic acid is an E. coli cell comprising an inactivated sialic acid transporter gene (nanT; encoding SEQ ID NO:14), an inactivated sialic acid aldolase gene (nanA; encoding SEQ ID NO:15), and an inactivated GlcNAc-6-P deacetylase gene (nagA; encoding SEQ ID NO:16); the recombinant cell also comprises a gene encoding H. pylori PseB (SEQ ID NO:1), a gene encoding H. pylori PseC (SEQ ID NO:2), a gene encoding H. pylori PseH (SEQ ID NO:3), a gene encoding H. pylori PseI (SEQ ID NO:4), a gene encoding C. jejuni PseG (SEQ ID NO:5), a gene encoding S. cerevisiae GlcNAc-6-P mutase (Agm1; SEQ ID NO:12), and the S. cerevisiae gene uap1 (encoding a GlcNAc-1-P uridyltransferase; SEQ ID NO:13); one specific, non-limiting example is construct BRL04/pBRL178/pBRL175, described herein. In another non-limiting example, the recombinant strain is IDAC deposit No. 060411-02.

Legionaminic acid, also referred to herein as “Leg”, “Leg5Ac7Ac”, or “5,7-diacetamido-3,5,7,9-tetradeoxy-D-glycero-D-galacto-nonulosonic acid”, is also a nine-carbon α-keto acid. Its structure is shown in FIG. 1. The recombinant cell for production of Leg comprises genes encoding PglF, PglE, PglD, LegG, and LegI enzyme function. By the term “encoding Pgl[ ]/Leg[ ] enzyme function”, also referred to herein as “Pgl[ ]/Leg[ ] genes”, it is meant that the genes encode an enzyme with a function equivalent to that of Pgl[ ]/Leg[ ]; these enzyme notations and their functions are described in Table 1 and FIG. 2. The Leg or Pgl genes inserted into the recombinant cell may be from any suitable source, including any biological source capable of producing legionaminic acid; for example, and without wishing to be limiting in any manner, the genes may be from C. jejuni, C. coli, L. pneumophila, Clostridium botulinum, E. coli O161, Acinetobacter baumannii, Pseudomonas fluorescens, Vibrio salmonicida, V. alginolyticus, V. parahaemolyticus, or any other suitable source. The recombinant cell for production of Leg also comprises genes encoding GlcNAc-6-P mutase and GlcNAc-1-P uridyltransferase (Table 2 and FIG. 2). The GlcNAc-6-P mutase and GlcNAc-1-P uridyltransferase genes may be from any suitable source; as would be known to those of skill in the art, many biological sources comprise GlcNAc-6-P mutase or GlcNAc-1-P uridyltransferase genes, and any of these may be used in the present invention. For example, and without wishing to be limiting in any manner, the genes may be from S. cerevisiae, C. albicans, Homo sapiens, Drosophila melanogaster, or any other suitable source.

Additionally, and similarly to the recombinant cell used for production of Pse, the recombinant cell used for production of Leg comprises an inactivated GlcNAc-6-P deacetylase gene, described in Table 2. As would be understood by those of skill in the art, the source of the inactivated genes will be dependent on the type of recombinant cell used. Optionally, the recombinant cell for producing Leg may either have an inactivated sialic acid transporter gene, an inactivated sialic acid aldolase gene, an inactivated ManNAc-6-P epimerase gene (for example, nanE), an inactivated undecaprenyl-P/UDP-GlcNAc transferase gene (for example, wecA), or a combination thereof. NanE may be responsible for depletion of intermediates in the Leg biosynthetic pathway (specifically 6-deoxy-MandiNAc), while WecA may be responsible for the depletion of intermediates in the Leg biosynthetic pathway (specifically UDP-BacdiNAc).

In a specific, non-limiting example, the recombinant cell for production of legionaminic acid is an E. coli cell comprising an inactivated sialic acid transporter gene (nanT; encoding SEQ ID NO:14), an inactivated sialic acid aldolase gene (nanA; encoding SEQ ID NO:15), an inactivated GlcNAc-6-P deacetylase gene (nagA; encoding SEQ ID NO:16), a gene encoding C. jejuni PglF (SEQ ID NO:6), a gene encoding C. jejuni PglE (SEQ ID NO:7), a gene encoding C. jejuni PglD (SEQ ID NO:8), a gene encoding C. jejuni LegI (SEQ ID NO:9), a gene encoding L. pneumophila LegG (SEQ ID NO:11), a gene encoding S. cerevisiae GlcNAc-6-P mutase (Agm1; SEQ ID NO:12), and the S. cerevisiae gene uap1 (encoding a GlcNAc-1-P uridyltransferase; SEQ ID NO:13). Optionally, the recombinant cell further comprises an inactivated ManNAc-6-P epimerase gene (nanE; encoding SEQ ID NO:17), an inactivated undecaprenyl-P/UDP-GlcNAc transferase gene (wecA; encoding SEQ ID NO:18), or a combination thereof.

The present invention further provides a cell-based fermentation method for the production of pseudaminic acid, comprising growing the recombinant cell as described above (for the production of Pse) and recovering the produced pseudaminic acid.

Similarly, the present invention provides a cell-based fermentation method for the production of legionaminic acid, comprising growing the recombinant cell as described above (for the production of Leg) and recovering the produced legionaminic acid.

By the term “cell-based fermentation method”, it is meant that microorganisms are used in a fermentation process; in the present case, the microorganisms are the recombinant cells of the present invention. The fermentation process may occur under aerobic or anaerobic conditions; specific methods and conditions for cell-based fermentation may vary based on the type of recombinant cell, and are well-known in the art. The fermentation process may also be conducted as either a batch or a continuous process. In the batch process, the recombinant cells are mixed in an aqueous suspension of growth medium and optionally supplements, and placed under an atmosphere that includes or excludes oxygen. In a continuous mode, the aqueous suspension of the recombinant cells and medium is circulated through the fermentor at a constant flow rate, such that the volume in the fermentation vessel is constant; at steady state, the growth rate of the cells is equal to the dilution rate.

The final product, legionaminic acid or pseudaminic acid, may be recovered from the culture medium or cell lysates by any suitable method known in the art. For example, and without wishing to be limiting in any manner, the legionaminic acid or pseudaminic acid may be recovered by conventional chromatography utilizing, for example, preparative fast performance liquid chromatography or high performance liquid chromatography (FPLC/HPLC) instruments, or recovered by precipitation and/or recrystallization approaches. In a batch fermentation process, the final product may be recovered at the end of the process; in a continuous process, the final product may be recovered continuously or at various time points.

The present invention also provides recombinant cells and methods for production of legionaminic and pseudaminic acid precursors, also referred to herein as UDP-2,4-diacetamido-2,4,6-trideoxy hexoses (UDP-DATDHs). Specifically, the present invention provides a recombinant cell for the production of UDP-DATDHs such as the pseudaminic acid biosynthetic precursor UDP-2,4-diacetamido-2,4,6-trideoxy-β-L-altropyranose (UDP-6-deoxy-AltdiNAc) and the legionaminic acid biosynthetic precursor UDP-2,4-diacetamido-2,4,6-trideoxy-α-D-glucopyranose (UDP-BacdiNAc).

UDP-2,4-diacetamido-2,4,6-trideoxy-β-L-altropyranose, also referred to herein as UDP-6-deoxy-AltdiNAc, is a pseudaminic acid biosynthetic precursor; it can be converted to Pse by the actions of PseG and PseI enzymes. The recombinant cell for production of UDP-6-deoxy-AltdiNAc comprises genes encoding PseB enzyme function, a gene encoding PseC enzyme function, and a gene encoding PseH enzyme function (Table 1 and FIG. 2); the recombinant cell for producing UDP-6-deoxy-AltdiNAc also comprises a gene encoding GlcNAc-6-P mutase and a gene encoding a GlcNAc-1-P uridyltransferase (Table 2 and FIG. 2). The source of the Pse genes described above may be from any suitable source, including a biological source capable of producing UDP-6-deoxy-AltdiNAc. For example, and without wishing to be limiting in any manner, the genes may be from H. pylori, C. jejuni, or any other suitable source. The source of the GlcNAc-6-P mutase gene, and the GlcNAc-1-P uridyltransferase genes inserted into the recombinant cell for the production of UDP-6-deoxy-AltdiNAc are as described above for the recombinant cell for the production of pseudaminic acid.

Additionally, the recombinant cell used for production of UDP-6-deoxy-AltdiNAc comprises an inactivated GlcNAc-6-P deacetylase gene, described in Table 2. Optionally, the recombinant cell used for production of UDP-6-deoxy-AltdiNAc comprises an inactivated sialic acid transporter gene, and/or an inactivated sialic acid aldolase gene. As would be understood by those of skill in the art, the source of the inactivated genes will be dependent on the type of recombinant cell used.

In a specific, non-limiting example, the recombinant cell for production of UDP-6-deoxy-AltdiNAc is an E. coli cell comprising an inactivated sialic acid transporter gene (nanT; encoding SEQ ID NO:14), an inactivated sialic acid aldolase gene (nanA; encoding SEQ ID NO:15), an inactivated GlcNAc-6-P deacetylase gene (nagA; encoding SEQ ID NO:16), a gene encoding H. pylori PseB (SEQ ID NO:1), a gene encoding H. pylori PseC (SEQ ID NO:2), a gene encoding H. pylori PseH (SEQ ID NO:3), a gene encoding S. cerevisiae GlcNAc-6-P mutase (Agm1; SEQ ID NO:12), and the S. cerevisiae gene uap1 (encoding a GlcNAc-1-P uridyltransferase; SEQ ID NO:13); one specific, non-limiting example is construct BRL04/pBRL178/pBRL151, described herein.

UDP-2,4-diacetamido-2,4,6-trideoxy-α-D-glucopyranose, also referred to herein as UDP-BacdiNAc, is a legionaminic acid biosynthetic precursor; UDP-BacdiNAc can be converted to Leg by the actions of LegG and LegI enzymes. The recombinant cell for production of UDP-BacdiNAc comprises genes encoding PglF, PglE, and PglD enzyme functions (Table 1 and FIG. 2); the recombinant cell for producing UDP-BacdiNAc also comprises a gene encoding GlcNAc-6-P mutase and a gene encoding a GlcNAc-1-P uridyltransferase (Table 2 and FIG. 2). The source of the Pgl genes described above may be from any suitable source, including a biological source capable of producing UDP-BacdiNAc. For example, and without wishing to be limiting in any manner, the genes may be from C. jejuni, L. pneumophila, or any other suitable source. The source of the GlcNAc-6-P mutase gene and the GlcNAc-1-P uridyltransferase gene inserted into the recombinant cell for the production of UDP-BacdiNAc are as described above for the recombinant cell for the production of legionaminic acid.

Additionally, the recombinant cell used for production of UDP-BacdiNAc comprises an inactivated GlcNAc-6-P deacetylase gene, described in Table 2. Optionally, the recombinant cell for producing UDP-BacdiNAc comprises an inactivated sialic acid transporter gene, and/or an inactivated sialic acid aldolase gene, and/or an inactivated undecaprenyl-P/UDP-GlcNAc transferase gene. As would be understood by those of skill in the art, the source of the inactivated genes will be dependent on the type of recombinant cell used.

In a specific, non-limiting example, the recombinant cell for production of UDP-BacdiNAc is an E. coli cell comprising an inactivated sialic acid transporter gene (nanT; encoding SEQ ID NO:14), an inactivated sialic acid aldolase gene (nanA; encoding SEQ ID NO:15), and an inactivated GlcNAc-6-P deacetylase gene (nagA; encoding SEQ ID NO:16); the recombinant cell also comprises a gene encoding C. jejuni PglF (SEQ ID NO:6), a gene encoding C. jejuni PglE (SEQ ID NO:7), and a gene encoding C. jejuni PglD (SEQ ID NO:8), a gene encoding S. cerevisiae GlcNAc-6-P mutase (Agm1; SEQ ID NO:12), and the S. cerevisiae gene uap1 (encoding a GlcNAc-1-P uridyltransferase; SEQ ID NO:13). The bacterial cell may additionally comprise an inactivated undecaprenyl-P/UDP-GlcNAc transferase gene (wecA; encoding SEQ ID NO:18); one specific, non-limiting example is construct BRL04/pBRL178/pBRL152, described herein. In another non-limiting example, the recombinant strain is IDAC deposit No. 060411-01.

The present invention also provides a cell-based fermentation method for the production of UDP-2,4-diacetamido-2,4,6-trideoxy-β-L-altropyranose (UDP-6-deoxy-AltdiNAc), comprising growing the recombinant cell as described above and recovering the produced UDP-6-deoxy-AltdiNAc.

The present invention further provides a cell-based fermentation method for the production of UDP-2,4-diacetamido-2,4,6-trideoxy-α-D-glucopyranose (UDP-BacdiNAc), comprising growing the recombinant cell as described above and recovering the produced UDP-BacdiNAc.

The enzymes and genes described in the above bacterial cells for the production of precursor compounds are as described previously above. Similarly, conditions for the methods just described are as indicated above for the production of the final products. Methods for recovering the products are as described herein.

The precursors, UDP-6-deoxy-AltdiNAc and UDP-BacdiNAc, obtained using the recombinant cells and methods above, may be converted to pseudaminic acid and legionaminic acid, respectively. Methods for conversion of these precursors to the final product are well known in the art. For example, UDP-6-deoxy-AltdiNAc may be converted to pseudaminic acid by incubation in a reaction vessel comprising a UDP-sugar hydrolase (PseG), a pseudaminic acid synthase (PseI), and phosphoenolpyruvate (PEP) or pyruvate. Alternatively, UDP-6-deoxy-AltdiNAc sugar could be converted to 6-deoxy-AltdiNAc with PseG, which may be chemically modified as described by Lee et al. (2010), to produce pseudaminic acid. As well, UDP-6-deoxy-AltdiNAc may be converted to 6-deoxy-AltdiNAc by chemical methods (such as heat or acidic treatment), and then converted to pseudaminic acid with PseI and PEP/pyruvate or the chemical methods described above. Similarly, UDP-BacdiNAc may be converted to legionaminic acid by incubating it in a reaction vessel comprising a UDP-sugar hydrolase and 2-epimerase (LegG), a legionaminic acid synthase (LegI) or sialic acid aldolase, and phosphoenolpyruvate (PEP) or pyruvate. Alternatively, the UDP-BacdiNAc may be converted to Leg by chemi-enzymatic methods similar to above (Tsvetkov et al., 2001).

Optionally, the Pse and Leg sugars produced by the methods described herein may be further converted to respective CMP-activated sugars with the CMP-pseudaminic acid synthetase (PseF; Schoenhofen et al, 2006a) and CMP-legionaminic acid synthetase (LegF; Schoenhofen et al, 2009), respectively. PseF catalyzes the reaction [CTP+pseudaminic acid→CMP-pseudaminic acid+pyrophosphate], whereas LegF catalyzes the reaction [CTP+legionaminic acid→CMP-legionaminic acid+pyrophosphate]. The conversion to CMP-sugars may be accomplished by any suitable method in the art, for example either by co-expression within recombinant cells (i.e. PseBCHGIF or PglFED/LegGIF strains), mixing of separate recombinant cells (i.e. PseBCHGI+PseF, or PglFED/LegGI+LegF), or by in vitro synthesis after their isolation (Pse or Leg) using methods known to those skilled in the art. The PseF and LegF enzymes may be from any suitable source; for example, and without wishing to be limiting in any manner, the genes may be from H. pylori, C. jejuni, C. coli, P. aeruginosa, L. pneumophila, or any other suitable source. Methods of producing such CMP-activated sugars are encompassed by the present invention.

To produce pseudaminic acid, the complete Pse-biosynthetic pathway and UDP-GlcNAc generating enzymes Agm1 and Uap1 were introduced into an E. coli strain (BRL02) previously engineered for the synthesis of sialic acid (Example 3). This system failed to produce significant levels of Pse or Pse-pathway intermediates. The extremely low productivity was attributed to the degradation of the Agm1/Uap1/PseBCHGI− pathway substrate, GlcNAc-6-P, via NagA (GlcNAc-6-P deacetylase). Therefore, the pseBCHGI and agm1/uap1 genes were introduced into the ΔnagA E. coli strain BRL04 (Example 3). However, co-transformation of the PseBCHGI pathway and Agm1/Uap1 proteins as a hepta-cistronic operon, encoded on a single vector (pBRL179), into the ΔnagA strain BRL04 failed to produce viable clones on every attempt. The pseBCHGI-agm1-uap1 operon is controlled by a T7 promoter, and it is widely accepted that leaky expression results from T7 promoters (Studier et al, 1990). The failure to co-transform the Pse-biosynthetic pathway and Agm1/Uap1 proteins into the ΔnagA strain BRL04 was due to a toxicity associated with the leaky expression of the pseBCHGI/agm1/uap1 genes. Independent transformations of either the pseBCHGI or agm1/uap1 genes were successful in generating viable clones, which indicated that neither pathway alone is toxic in the ΔnagA strain. Only a combination of both sets of genes was required for toxicity (Example 3). By splitting the hepta-cistronic PseBCHGI/Agm1/Uap1 system into two operons, pseBCHGI and agm1/uap1, on two separate, T7-controlled expression vectors (pBRL175 and pBRL178) with different replication origins, viable BRL04/pseBCHGI/agm1/uap1 clones were generated. Analysis of cell-free culture broth from these BRL04/pseBCHGI/agm1/uap1 cells 4A) indicated pseudaminic acid production (Example 3).

The sub-optimal production of the Pse product and pathway intermediates in some engineered strains (BRL02, BL21(DE3), BRL25; Examples 3 and 5) suggested that either the acetyl-CoA levels were suboptimal due to an additional N-acetylation required relative to sialic acid biosynthesis; that the intermediates in the Pse-biosynthetic pathway were being consumed by undesirable intracellular glycosylation reactions; or that intermediates were degraded by unidentified mechanisms. Removal of all non-essential glycosylation reactions in the engineered E. coli strain (BRL25) did not have an effect on the production of pseudaminic acid (Example 5).

The only dissimilation pathway in E. coli K-12 for 2-acetamido sugars (Plumridge & Vimr, 1999) involves a highly specific process that includes a deacetylase, NagA, and a deaminase, NagB (Plumridge & Vimr, 1999). The deacetylase, NagA, removes the acetate at C2 of N-acetyl glucosamine-6-phosphate (GlcNAc-6-P) to generate glucsosamine-6-phosphate (GlcN-6-P); NagB then deaminates GlcN-6-P into fructose-6-phosphate, which then enters central metabolism. This pathway may be responsible for catabolizing the Pse-biosynthetic pathway intermediates, which have the same configuration at C2, thus preventing the production of pseudaminic acid. Only when the GlcNAc-6-P deacetylase, NagA, was deleted was Pse readily produced (Example 3). It is therefore possible that the native E. coli pathway for the degradation of N-acetylglucosamine is in fact able to catabolize 2-acetamido-6-deoxy hexoses such as 2,4-diacetamido-2,4,6-trideoxy-L-altropyranose (6-deoxy-AltdiNAc).

The present invention will be further illustrated in the following examples. However, it is to be understood that these examples are for illustrative purposes only and should not be used to limit the scope of the present invention in any manner.

Example 1 Construction of Recombinant Pathway for Pseudaminic Acid, UDP-6-Deoxy-AltdiNAc, and UDP-BacdiNAc Biosynthesis

Plasmids encoding the H. pylori pseB, pseC, pseH and pseI genes, and the C. jejuni pseG gene were provided by the Institute for Biological Sciences, National Research Council (Ottawa, Ontario, Canada). The plasmids were used as templates for PCR with the primers given in Table 3. Initial constructions of H. pylori pseB, pseC, pseH and pseG genes (in a pseBCHGI operon) examined via Western blot of cell lysates showed that the H. pylori PseB, PseC and PseH were successfully expressed but not PseG (data not shown). Therefore, the C. jejuni PseG was cloned and used in place of H. pylori PseG.

The pglF, pglE and pglD genes were amplified from C. jejuni (ATCC® 700819-5) genomic DNA using primers also shown in Table 3.

TABLE 3 Forward (f) and reverse (r) primers used for amplification of pse and pgl genes, shown with restriction sites. Primers (m1, m2) used for the mutagenesis of pseB to remove internal EcoRI site are given. pseB f-gcagcatatgccaaatcatcaaaacatgctag SEQ ID NO: 19 Nde I r-gcaggaattctcataataatttcaacaaatcatcaggctc SEQ ID NO: 20 EcoRI m1-ccatttagccctagagttcgaagactttttcatcattcagccc SEQ ID NO: 21 m2-gggctgaatgatgaaaaagtcttcgaactctagggctaaatgg SEQ ID NO: 22 pseC f-gcagcatatgaaagagtttgcttatagcgag SEQ ID NO: 23 Nde I r-gcaggaattctcattctattttaaaactctcaaaag SEQ ID NO: 24 EcoR I pseH f-gcagcatatgaaaaaaaattattcttataaaaatatccaagcgattg SEQ ID NO: 25 Nde I r-gcaggaattcctaaagttttagaagagattgatcattatatc SEQ ID NO: 26 EcoR I pseG f-ggaccatatgaaagtgctttttagaagcgatagc SEQ ID NO: 27 Nde I r-ggacgaattctcaatacttatactccacttcataccc SEQ ID NO: 28 EcoR I pseI f-gcagcatatgttacaaccccctaaaattgtc SEQ ID NO: 29 Nde I r-gcaggaattcctacaatgagcgttctatatcatc SEQ ID NO: 30 EcoR I pglF f-gcagcatatgattttttataaaagcaaaagattagca SEQ ID NO: 31 Nde I r-gcaggaattcttatacaccttctttattgtgtttaaattc SEQ ID NO: 32 EcoR I pglE f-gcagcatatgagattttttctttctcctccgcacatgggtggtaatg SEQ ID NO: 33 Nde I r-gcaggaattcttaagcctttatgctctttaagatcagttttga SEQ ID NO: 34 EcoR I pglD f-gcagcatatggcaagaactgaaaaaatttatatttatgg SEQ ID NO: 35 Nde I r-gcaggaattcttacatcctttttgcaggtactcc SEQ ID NO: 36 EcoR I

The PCR products were cloned into various plasmids, including pCR-Blunt (Invitrogen, Carlsbad, Calif.) and plasmid pKH22 (Lundgren and Boddy, 2007; Table 7). The sub-cloning of genes and construction of recombinant expression vectors described in this and following Examples was done using standard molecular biology techniques (Erbel et al, 2003).

A full pseudaminic acid biosynthetic pathway was constructed using genes encoding the proteins PseB (HP0840; SEQ ID NO:1), PseC (HP₀₃₆₆; SEQ ID NO:2), PseH (HP₀₃₂₇; SEQ ID NO:3), and PseI (HP0178; SEQ ID NO:4) from H. pylori and PseG (Cj1312; SEQ ID NO: 5) from C. jejuni. This set of enzymes was shown to synthesize Pse from UDP-GlcNAc in vitro (Schoenhofen et al, 2006a). The pseBCHGI operon was constructed by sequentially cloning the Xba I-Avr II fragment of the targeted downstream gene(s) into the Avr II of the parental vector, yielding a low-copy expression vector and arranged into a penta-cistronic operon, controlled by a single T7 promoter (pBRL175; Table 4).

The UDP-6-deoxy-AltdiNAc biosynthetic pathway was constructed using genes encoding the proteins PseB (HP0840; SEQ ID NO:1), PseC (HP0366; SEQ ID NO:2), and PseH (HP0327; SEQ ID NO:3) from H. pylori. This set of enzymes was shown to synthesize UDP-6-deoxy-AltdiNAc from UDP-GlcNAc in vitro (Schoenhofen et al, 2006a; Schoenhofen et al, 2006b). Construction of the pseBCH operon was achieved by sequentially cloning the Xba I-Avr II fragment of the targeted downstream gene(s) into the Avr II of the parental vector, resulting in a low-copy expression vector and arranged into a tri-cistronic operon, controlled by a single T7 promoter (pBRL151, Table 4).

The UDP-BacdiNAc biosynthetic pathway was constructed using genes encoding the proteins PglF (Cj1120c SEQ ID NO:6), PglE (Cj1121c SEQ ID NO:7), and PglD (Cj1123c SEQ ID NO:8) from C. jejuni. This set of enzymes was shown to synthesize UDP-BacdiNAc from UDP-GlcNAc in vitro (Schoenhofen et al, 2006b; Oliver et al, 2006). Construction of the pglFED operon was achieved by sequentially cloning the Xba I-Avr II fragment of the targeted downstream gene(s) into the Avr II of the parental vector, resulting in a low-copy expression vector and arranged into a tri-cistronic operon, controlled by a single T7 promoter (pBRL152, Table 4).

Resulting plasmids, listed in Table 4, may be used for the biosynthesis of pseudaminic acid (Pse), legionaminic acid (Leg) and their precursors UDP-6-deoxy-AltdiNAc and UDP-BacdiNAc, respectively.

TABLE 4 Plasmids used for the production of UDP-GlcNAc, pseudaminic acid (Pse), UDP-2,4-diacetamido-2,4,6-trideoxy-α-D-glucopyranose (UDP-BacdiNAc) and UDP-2,4-diacetamido-2,4,6-trideoxy-β-L- altropyranose (UDP-6-deoxy-AltdiNAc) Biosynthesized Plasmid Operon Metabolite pBRL179 pseBCHGI-agm1-uap1 Pse See Example 3 pBRL175 pseBCHGI Pse See Example 3 pBRL151 pseBCH UDP-6-deoxy- See Example 4 AltdiNAc pBRL152 pglFED UDP-BacdiNAc See Example 4 pBRL178 agm1-uap1 UDP-GlcNAc See Example 3

Example 2 Cloning of a UDP-GlcNAc Biosynthetic Pathway

The Pse-biosynthetic pathway diverges from E. coli metabolism at the key branch point UDP-GlcNAc, the synthesis of which is tightly regulated by homeostatic mechanisms (Plumbridge et al, 1993). To circumvent the dependency of Pse/Leg or UDP-6-deoxy-AltdiNAc/UDP-BacdiNAc production from UDP-GlcNAc supplied only by homeostasis, a foreign, yeast-derived UDP-GlcNAc biosynthetic pathway was co-expressed with the Pse or UDP-6-deoxy-AltdiNAc/UDP-BacdiNAc biosynthetic pathways.

The genes encoding the enzymes for a GlcNAc-6-P mutase (Hofmann et al, 1994), Agm1 (SEQ ID NO:12), and a GlcNAc-1-P uridyltransferase (Mio et al, 1998), Uap1 (SEQ ID NO:13), were cloned from Saccharomyces cerevisiaie. For E. coli, exogenously-fed GlcNAc is taken up by PTS-transporters, i.e., ManXYZ and/or NagE (GlcNAc-inducible), to generate intracellular GlcNAc-6-P, which can only be degraded into Fru-6-P in wild-type E. coli. Expression of the non-native Agm1/Uap1 pathway enabled GlcNAc-6-P to be directly converted to UDP-GlcNAc, bypassing E. coli central metabolism and generating higher pools of UDP-GlcNAc for Pse, Leg, UDP-BacdiNAc, and UDP-6-deoxy-AltdiNAc production.

The agm1 (GlcNAc-6-P mutase) and uap1 (GlcNAc-1-P uridyltransferase) from S. cerevisiae were previously cloned into the expression vector pKH22 as a bi-cistronic operon controlled by a T7-promoter, thus generating the plasmid pBRL80 (Lundgren, 2010). This system was highly productive in converting exogenously supplied GlcNAc into UDP-GlcNAc (Lundgren, 2010).

The Xba I/Avr II agm1-uap1 fragment from pBRL80 was sub-cloned into either the Avr II site of pBRL175 (pseBCHGI) or the Xba I site of pKH61 (Lundgren, 2010) to generate plasmids pBRL179 and pBRL178, respectively (Lundgren, 2010). The vector pBRL179 encoded all the necessary genes for channelling GlcNAc into Pse production. In contrast, the pBRL178 supplied only the agm1-uap1 genes but could be readily co-expressed with the plasmid-encoded pathways for UDP-6-deoxy-AltdiNAc (pseBCH on pBRL151), Pse (pseBCHGI on pBRL175), or UDP-BacdiNAc (pglFED on pBRL152), or Leg.

Example 3 Pseudaminic Acid Production from E. Coli

For initial Pse production experiments, the PseBCHGI pathway was expressed in the commercially available, industrially-friendly E. coli BL21(DE3) strain. Chemical transformation of plasmids into cells was performed using art-known methods. Because there was no known Pse-specific aldolase or degradation pathway for 2-acetamido-6-deoxy sugars encoded in the E. coli genome (Lewis et al, 2009), E. coli BL21(DE3) served as a desirable host for Pse production due to its robustness in gene expression. However, the BL21(DE3)/PseBCHGI strain failed to produce any detectable Pse from either glycerol or glucose batch fermentation (data not shown). Expression of the non-native pseBCHGI genes was not an issue, because the Pse-biosynthetic proteins were detected by Western blots of production-culture cell lysates derived from both minimal and complex media (data not shown).

The Pse-biosynthetic pathway along with the Agm1 and Uap1 genes (pBRL179, Example 1) were transformed into and co-expressed in the nanT⁻ nanA⁻ E. coli strain BRL02 (Table 6) using method known in the art; this strain was previously engineered for sialic acid production (Lundgren & Boddy, 2007). Pse production was performed using a mixed feeding strategy of glycerol/GlcNAc batch fermentations in shake-flasks. Glycerol supplied the cells with energy and biosynthetic precursors whereas GlcNAc fed into UDP-GlcNAc synthesis for Pse production.

Briefly, starter cultures were grown in 1 mL of LB media, supplemented with the necessary antibiotics, at 37° C., 200 rpm, for 18 h. A 20 mL F2 minimal media (in 250-mL shake-flask), supplemented with the necessary antibiotics, 0.25% casitone and 1% (v/v) glycerol was inoculated with 0.2 mL of starter culture. Production cultures were grown at 37° C., 200 rpm, until an OD₆₀₀ of 0.5 was reached. At this point, pseudaminic acid production was induced with 0.2 mM IPTG (final concentration), and the incubation temperature was lowered to 30° C. Production cultures were grown for 72 h and supplemented with 0.6% (v/v) glycerol at 0, 12 and 36 h post induction. At 0, 18 and 36 h post induction, doses of 0.2% GlcNAc were added for pseudaminic acid biosynthesis/production.

Expression of the hepta-cistronic operon of pBRL179 in E. coli strain BRL02 produced a trace amount of Pse with m/z of 317 (M−OH), 335 (M+H), and 357 (M+Na), see FIG. 3. The extremely low productivity was attributed to the degradation of the Agm1/Uap1/PseBCHGI-pathway substrate, GlcNAc-6-P, via NagA (GlcNAc-6-P deacetylase; SEQ ID NO: 16).

Therefore, the pseBCHGI and agm1/uap1 genes in pBRL179 were introduced into the nanT nanA⁻ ΔnagA⁻ E. coli strain BRL04 (Table 6); chemical transformation of plasmids into cells was performed using art-known methods. Cell culture and gene expression were performed as described above. Co-transformation of the PseBCHGI pathway and Agm1/Uap1 proteins as a hepta-cistronic operon encoded on a single vector, into the ΔnagA strain BRL04 failed to produce viable clones on every attempt. The pseBCHGI-agm1-uap1 operon is controlled by a T7 promoter, and it is widely accepted that leaky expression results from T7 promoters (Studier et al, 1990). The failure to co-transform the Pse-biosynthetic pathway and Agm1/Uap1 proteins into the ΔnagA strain BRL04 was due to a toxicity associated with the leaky expression of the pseBCHGI/agm1/uap1 genes.

Independent transformations of either the pseBCHGI (in pBRL175) or agm1/uap1 genes (in pBRL178) using art-known chemical transformation methods were successful in generating viable clones (data not shown), indicating that neither pathway alone is toxic in the nanT⁻ nanA⁻ΔnagA strain. Based on these results and those of Example 4, BRL04 cells were transformed with pseBCHGI (in pBRL175) and agm1/uap1 (in pBRL178) using art-known chemical transformation methods, generating viable BRL04/pseBCHGI/agm1/uap1 clones (strain BRL04/pBRL178/pBRL175). This clone was deposited with the International Depositary Authority of Canada (National Microbiology Laboratory, Public Health Agency of Canada, 1015 Arlington Street, Winnipeg, Manitoba, Canada R3E 3R2) on Apr. 7, 2011, under deposit number 060411-02.

Cell culture and gene expression were performed as described above. The pseBCHGI and agm1/uap1 genes were present on plasmids with copy numbers (replication origins) of ˜20 (pMB1*) and >100 (mutated ColE1), respectively (Hayes, 2003). Under non-induced conditions, the substantially higher copy number of the uap1/agm1 operon out-competed the pseBCHGI pathway for T7-polymerase mediated transcription. This increased the synthesis of UDP-GlcNAc but did not raise its flux through Pse biosynthesis, thus keeping Pse-pathway intermediates at non-toxic levels.

The cell-free culture broth was analyzed using a LCMS ESI⁺ method developed herein (see Example 4). Analysis of cell-free culture broth from BRL04/pseBCHGI/agm1/uap1 cells (strain BRL04/pBRL178/pBRL175) in a glycerol/GlcNAc-batch fermentation by LCMS ESI⁺ (FIG. 4A) showed a clear ion-extraction peak for Pse with m/z values of 317(M−OH), 335 (M+H) and 357 (M+Na). These ion extraction peaks were not present in the negative control production culture (data not shown). To confirm that these m/z values were derived from authentic Pse, cell-free broth from the negative control culture was spiked with Pse standard. As shown in FIGS. 4A and B, the ion-extraction peak of the spiked sample was identical to the Pse produced from the BRL04/pseBCHGI/agm1/uap1 fermentation (strain BRL04/pBRL178/pBRL175). Although a quantitative Pse titer could not be determined, a rough estimate based on the inability to detect Pse standards injected at concentrations of <40 mg L⁻¹, would imply that Pse production was at least ≧20 mg L⁻¹. Quantitative determination of Pse titers can be made by analyzing pseudaminic acid from cell-free culture broth derivatized with the fluormetric reagent, 1,2-diamino-4,5-methylene dioxybenzene (DMB) by HPLC (Lewis et al, 2009; Manzi et al, 1990). This assay is widely used for sialic acid quantification and has been applied to Pse (Lewis et al, 2009).

The production of Pse was further optimized by increasing the acetyl-CoA pools in the nanT⁻ nanA⁻ ΔnagA E. coli strain BRL04. Unlike sialic acid, Pse biosynthesis involves a diacetamido sugar that is generated from a dedicated acetyl-CoA dependent acetyltransferase, PseH. To increase the acetyl-CoA levels in BRL04/pseBCHGI/agm1/uap1 through β-oxidation, cell culture of BRL04 transformed with pBRL175 and pBRL178 was grown and gene expression was performed as described above except that production cultures were supplemented with 0.6 mg L⁻¹ of palmitate. As indicated in FIG. 5, Pse was readily produced and appeared to be higher than that without palmitate addition. This suggested that acetyl-CoA may be a factor for the production of diacetamido sugars in E. coli.

Example 4 Analysis of Pseudaminic Acid and Legionaminic Acid from Cell-Free Culture Broth Via LCMS ESI⁺

Due to the failures with Pse detection using proton NMR, a LCMS ESI⁺ method was developed and validated to detect Pse from production cultures of Example 3 (FIG. 6).

Briefly, cell-free broth from production cultures (Example 3) were diluted 100-fold into 0.1 mL of water and analyzed by LCMS ESI⁺ (10 μL injection volumes) on a Shimadzu LCMS 2010A. HPLC conditions: UV detection λ=210, 254 nm, Thermo 50×4.6 mm, 3 μm, Hypercarb® HPLC column (graphitic carbon based packing), flow rate 0.15 mL/min, isocratic elution H₂O, 0.05% v/v formic over 20 min run time.

Example 5 Production of UDP-Activated 2,4-diacetmido-2,4,6-Trideoxy Hexoses from E. Coli

Plasmids pBRL151 (pseBCH) or pBRL152 (pglFED) (Example 1; Table 4), encoding the biosynthetic pathways for the Pse precursor UDP-6-deoxy-AltdiNAc or Leg precursor UDP-BacdiNAc (FIG. 7), respectively, were transformed with pBRL178 (agm1-uap1; Example 2; Table 4) in the nanT⁻ nanA⁻ nagA⁻ E. coli strain BRL04 (Table 6; WO 2008/097366) using art-known chemical transformation methods. The BRL04/pBRL178/pBRL173 strain was used as a negative control.

To maximize cell density for the production of the UDP-DATDHs from shake-flasks, starter cultures were scaled up in 5-fold increments. Seed cultures of BRL04/pBRL178/pBRL151 or BRL04/pBRL178/pBRL152 were grown in 1 mL LB supplemented with appropriate antibiotics at 37° C., 200 rpm, for 18 h. Afterwards, entire seed cultures were harvested, and the resulting cell pellets were re-suspended and diluted into 5 mL of LB with necessary antibiotics. Cultures were grow at 37° C., 200 rpm, for 18 h and then re-harvested. Cell pellets were used to inoculate 20 mL LB with appropriate antibiotics and grown at 37° C., 200 rpm, for 18 h. At this time, the entire 20 mL seed culture was harvested, and the cell mass was used to inoculate the production culture of 100 mL 2XYT (in 2-L flasks) supplemented with 0.5% (v/v) glycerol and necessary antibiotics. Production cultures were grown at 30° C., 250 rpm, until an OD₆₀₀ of 5 was reached. At this point, UDP-DATDH production was induced with the addition of 0.3 mM IPTG (final concentration), and cultures were grown at 30° C., 250 rpm, for 60 h. At t=0, 12 and 36 h post induction, 0.5% (v/v) glycerol was added to the production cultures. To maximize UDP-DATDH production, doses of 0.3% GlcNAc were supplied at t=0, 12, 24 and 36 h post induction. At the end of the duration of the experiment, cultures were harvested and the resulting cell pellets were analyzed by capillary-electrophoresis-MS.

To determine if the nanT⁻ nanA⁻ ΔnagA E. coli strain can at least generate the necessary UDP-linked DATDH sugar for pseudaminic and legionaminic acid production, the agm1/uap1 and pseBCH or pglFED genes were co-expressed in BRL04 as described. Analysis of clarified-cell lysates from production cultures of BRL04/pBRL178/pBRL151 with CE-MS in the negative-ion mode gave a distinct m/z peak at 630.9 (M−H) for UDP-6-deoxy-AltdiNAc (FIG. 8A). This peak was absent in the negative control (FIG. 8C). Similarly, the BRL04/pBRL178/pBRL152 strain was shown to produce UDP-BacdiNAc (FIG. 8B; m/z of 630.9). These results confirmed that the engineered E. coli strains are able to synthesize and produce UDP-linked 2,4-diacetmido-2,4,6-trideoxy hexoses.

The strain for production of UDP-BacdiNAc, BRL04/pBRL178/pBRL152, was deposited with the International Depositary Authority of Canada (National Microbiology Laboratory, Public Health Agency of Canada, 1015 Arlington Street, Winnipeg, Manitoba, Canada R3E 3R2) on Apr. 7, 2011, under deposit number 060411-01.

Example 6 Construction of an E. Coli Strain Deficient in Enterobacterial Common Antigen (ECA), Colanic Acid, and Poly-N-Acetylglucosamine Biosynthesis

There are no known biosynthetic or catabolic enzymes in E. coli involved in the metabolism of 2-acetamido-6-deoxy sugars (Keseler et al, 2009). However, the UDP-GlcNAc undecaprenyl-phosphate transferase, WecA (SEQ ID NO:18), from E. coli K-12 has been shown to accept UDP-linked 2,4-diacetamido-2,4,6-trideoxy hexoses (Linton et al, 2005). This evidence indicates that E. coli could salvage UDP-activated 2-acetamido-6-deoxy sugars by incorporating them into its own exo-polysaccharides; however, the substrate specificities of the glycosyltransferases in the majority of these pathways are poorly characterized (FIG. 9). To prevent unwanted glycosylation reactions that could consume UDP-linked Pse intermediates, the genes necessary for the biosynthesis of colanic acid (Stevenson et al, 1996), enterobacterial common antigen (ECA; Erbel et al, 2003), and poly-N-acetyl glucosamine (PGA; Itoh et al, 2008), and wecA were deleted from E. coli K-12 to test the effect on Pse production. It is worth noting that WecA may have the same effect on a strain for the production of legionaminic acid.

A wecA⁻ E. coli K-12 strain was obtained from the Keio Collection; this strain, BW25113 (Δ(araD-araB)567, ΔlacZ4787(::rrnB-3), lambda-, rph-1, Δ(rhaD-rhaB)568, hsdR514) (Table 6), has the wecA gene replaced with a kanamycin marker, and thus cannot biosynthesize ECA.

A λ(DE3) lysogen, encoding a T7 RNA polymerase under the control of a lac promoter, was inserted into the chromosome of the wecA⁻ E. coli K-12 strain, using the λ(DE3) lysogenization kit from Novagen (San Diego, Calif.), to generate the strain BRL11. Next, the entire colanic acid and poly-N-acetyglucosamine gene clusters were sequentially deleted from BRL11 using the lambda Red system. The plasmids pKD3, pCP20 and pKD46, were used for lambda Red recombination in E. coli (Lundgren, 2010). Primers used for the construction of the replacement, antibiotic-marker cassettes are given in Table 5.

TABLE 5 Primers used for cassette construction. Primers (a1, a2) and (b1, b2) were used to PCR-amplify gene regions targeted for chromosomal deletion; primers (c1, c2) were used to generate the chloramphenicol-marker. The homology arms from (a1, a2) and (b1, b2) were fused with the marker from (c1, c2) to yield the full-length replacement cassette for lambda Red recombination. colanic a1-gttatcgatgatcaggttgcgc SEQ ID NO: 37 acid a2-gaagcagctccagcctacaccgccagcttgctgcaggctttatag SEQ ID NO: 38 b1-ctaaggaggatattcattgtttatttatcactttggcag SEQ ID NO: 39 b2-gtaataacctcacattatccctg SEQ ID NO: 40 c1-gtgtaggctggagctgcttc SEQ ID NO: 41 c2-gtgtaggctggagctgcttc SEQ ID NO: 42 pgaDABC a1-atgtattcaagtagcagaaaaaggtg SEQ ID NO: 43 a2-gaagcagctccagcctacacggttattgctgagtgctgattttagtgc SEQ ID NO: 44 b1-ctaaggaggatattcatgtctgggcgctgtacaataagctgcg SEQ ID NO: 45 b2-ttatgcccggactagcgctttttctgaaac SEQ ID NO: 46 c1-gtgtaggctggagctgcttc SEQ ID NO: 47 c2-atgggaattagccatggtcc SEQ ID NO: 48

Deletions were performed using standard molecular biology protocols. The colanic acid gene cluster region, wza-wcaM, was targeted first for deletion in the strain BRL11 and positive clones, were verified by kanamycin and chloramphenicol sensitivity. This markerless AwecA Δwza-wcaM E. coli strain was designated as BRL21.

The poly-N-acetylglucosamine gene cluster, pgaABCD (Rice et al, 2008), was then deleted from BRL21 to generate strain BRL25. The pgaABCD region was replaced with a chloramphenicol marker.

Expression of the PseBCHGI pathway in the biofilm deficient strain BRL25 did not yield any pseudaminic acid by proton NMR. The inability to detect Pse was attributed to a low conversion rate of UDP-GlcNAc into the desired pseudaminic acid product.

Example 7 Legionaminic Acid Production from E. Coli

Legionaminic acid is produced by co-expressing the pglFED (pBRL152) and agm1/uap1 (pBRL178) genes with the genes LegG and LegI (see Table 1) in E. coli BRL04. The LegG gene is derived from Legionella pneumophila (Glaze et al, 2008) (Lpg0753; SEQ ID NO:11) and the LegI gene is derived from C. jejuni (Schoenhofen et al, 2009) (Cj1327; SEQ ID NO:9) or L. Pneumophila (Glaze et al, 2008) (Lpg0752; SEQ ID NO:10).

Starter cultures are grown in 1 mL of LB media, supplemented with the necessary antibiotics, at 37° C., 200 rpm, for 18 h. A 20 mL F2 minimal media (in 250-mL shake-flask), supplemented with the necessary antibiotics, 0.25% casitone and 1% (v/v) glycerol is inoculated with 0.2 mL of starter culture. Production cultures are grown at 37° C., 200 rpm, until an OD₆₀₀ of 0.5 is reached. Legionaminic acid production is induced with 0.2 mM IPTG (final concentration), and the incubation temperature is lowered to 30° C. Production cultures are grown for 72 h and supplemented with 0.6% (v/v) glycerol at 0, 12 and 36 h post induction. At 0, 18 and 36 h post induction, doses of 0.2% GlcNAc are added for legionaminic acid biosynthesis/production.

Alternatively, pglFED (pBRL152) is co-expressed with agm1/uap1 (pBRL178) as just described above. To produce legionaminic acid, the expression is done in the presence of a UDP-BacdiNAc hydrolyzing 2-epimerase and a Leg synthase (Schoenhofen et al, 2009; Glaze et al, 2008). In yet another alternative, the UDP-BacdiNAc is recovered or partially recovered from the UDP-BacdiNAc culture of Example 5 and the UDP-BacdiNAc hydrolyzing 2-epimerase and Leg synthase enzymes are added to the recovered or partially recovered precursor.

As shown in FIGS. 2 and 10, an epimerase hydrolyzes the glycosidic linkage of UDP-BacdiNAc and catalyzes an inversion of configuration at C2 to liberate 2,4-diacetamido-2,4,6-trideoxy-D-mannose. Unlike the pseudaminic acid DATDH-biosynthetic intermediate 6-deoxy-AltdiNAc, which has the glucose configuration at C2 (FIG. 2), the Leg-DATDH precursor 6-deoxy-MandiNAc is unlikely to be catabolized by NagA/NagB. Instead, its degradation could proceed through N-acetylmannose metabolism consisting of the ManNAc-6-P epimerase, NanE (SEQ ID NO:17) (Plumbridge & Vimr, 1999). NanE converts ManNAc-6-P into GlcNAc-6-P, and thus is required for catabolism of 2-acetamido mannose sugars in E. coli. Thus, a strain for production of legionaminic acid could also comprise an inactivated ManNAc-6-P epimerase gene.

Detection of Leg from production cultures may be done using a method similar to that described in Example 10.

Example 8 Summary of Plasmids and E. Coli Strains

The bacterial strains and plasmids used and prepared herein are described in Tables 1 and 2, respectively.

TABLE 6 E. coli strains used given with relevant genotypes. The BRL02, BRL04 and BRL10 strains are derived from E. coli K-12 MG1655 (Kang et al, 2004). The BRL11, BRL21 and BRL25 strains are derived from E. coli BW25113. Resistance of strains to antibiotics kanamycin (Km), tetracycline (Tc) and/or chloramphenicol (Cm) is indicated. Strain Relevant Genotype Source Marker BL21(DE3) F-, ompT, hsdSB(rB-, mB-), dcm, gal, Novagen λ(DE3) BW25113 Δ(araD-araB)567, ΔlacZ4787(::rrnB-3), The Keio lambda-, rph-1, Δ(rhaD-rhaB)568, hsdR514 Collection BRL02 nanT::Tn5(kan)-l-SceI nanA:tet λ(DE3) WO2008/097366 Km, Tc BRL04 BRL02 ΔnagA WO2008/097366 Km, Tc, BRL11 BW25113 wecA ::kan λ(DE3) Km BRL21 BW25113 ΔwecA Δwza-wcaM λ(DE3) BRL25 BW25113 ΔwecA Δwza-wcaM pgaABCD::cat Cm λ(DE3)

TABLE 7 Plasmids constructed for the cloning and expression of the pseBCHGI and pglFED. Inserted Parental Antibiotic Plasmid Gene Vector Marker Origin of Inserted Gene pNRC8.1 pseB pCR-Blunt Km^(R) PCR product pNRC37.1 pseC pKH22 Am^(R) Nde I/EcoR I glmU of pBRL35 pNRC129.2 pseH pCR-Blunt Km^(R) PCR product pNRC133.1 pseG pBRL78 Km^(R) Mutagenesis of pBRL78 pNRC36.3 pseI pKH22 Am^(R) Nhe I/EcoR I of pBRL79 pBRL90 pseB pCR-Blunt Km^(R) PCR product pBRL91 pseC pCR-Blunt Km^(R) PCR product pBRL92 pseH pCR-Blunt Km^(R) PCR product pBRL94 pseI pCR-Blunt Km^(R) PCR product pBRL95 pseB pCR-Blunt Km^(R) Mutagenesis of pBRL90 pBRL97 pseC pKH22 Am^(R) Nde I/EcoR I pseC of pBRL91 pBRL98 pseH pKH22 Am^(R) Nde I/EcoR I pseH of pBRL92 pBRL99 pseI pKH22 Am^(R) Nde I/EcoR I pseI of pBRL94 pBRL100 pseB pKH22 Am^(R) Nde I/EcoR I pseB of pBRL95 pBRL143 pglF pKH22 Am^(R) Nde I/EcoR I pglF of pBRL133 pBRL144 pglD pKH22 Am^(R) Nde I/EcoR I pglD of pBRL135 pBRL145 pglE pKH22 Am^(R) Nde I/EcoR I pglE of pBRL134 pBRL146 pseC pBRL100 Am^(R) Xba I/Avr II pseC of pBRL97 pBRL149 pglE pBRL143 Am^(R) Xba I/Avr II pglE of pBRL145 pBRL151 pseH pBRL146 Am^(R) Xba I/Avr II pseH of pBRL98 pBRL152 pglD pBRL149 Am^(R) Xba I/Avr II pglD of pBRL141 pBRL171 pseG pCR-Blunt Km^(R) PCR product pBRL173 pseG pKH22 Am^(R) Nde I/EcoR I pseG of pBRL171 pBRL174 pseG pBRL151 Am^(R) Xba I/Avr II pseG of pBRL173 pBRL175 pseI pBRL174 Am^(R) Xba I/Avr II pseI of pBRL99 pBRL178 agm1-uap1 pKH61 pBRL179 agm1-uap1 pBRL175

The embodiments and examples described herein are illustrative and are not meant to limit the scope of the invention as claimed. Variations of the foregoing embodiments, including alternatives, modifications and equivalents, are intended by the inventors to be encompassed by the claims. Furthermore, the discussed combination of features might not be necessary for the inventive solution.

REFERENCES

All patents, patent applications and publications referred to herein and throughout the application are hereby incorporated by reference in their entirety.

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1. A recombinant cell for the production of pseudaminic acid, comprising an inactivated GlcNAc-6-P deacetylase gene, a gene encoding PseB enzyme function, a gene encoding PseC enzyme function, a gene encoding PseH enzyme function, a gene encoding PseI enzyme function, a gene encoding PseG enzyme function, a gene encoding a GlcNAc-6-P mutase, and a gene encoding a GlcNAc-1-P uridyltransferase.
 2. (canceled)
 3. The recombinant cell of claim 1, further comprising at least one of an inactivated nanT sialic acid transporter gene, an inactivated nanA sialic acid aldolase gene or a gene encoding an acetyl-CoA synthase.
 4. (canceled)
 5. (canceled)
 6. The recombinant cell of claim 1, wherein the recombinant cell is an E. coli cell and comprises an inactivated nanT sialic acid transporter gene, an inactivated nanA sialic acid aldolase gene, an inactivated nagA GlcNAc-6-P deacetylase gene, a PseB gene encoding SEQ ID NO:1, a PseC gene encoding SEQ ID NO:2, a PseH gene encoding SEQ ID NO:3, a PseI gene encoding SEQ ID NO:4, a PseG gene encoding SEQ ID NO:5, the agm1 GlcNAc-6-P mutase gene, and the uap1 GlcNAc-1-P uridyltransferase gene.
 7. The method of claim 20, wherein growth medium for the recombinant cell is supplemented with palmitate.
 8. (canceled)
 9. The recombinant cell for the production of pseudaminic acid of claim 1, wherein the cell is that of IDAC deposit No. 060411-02.
 10. A recombinant cell for the production of legionaminic acid, comprising an inactivated GlcNAc-6-P deacetylase gene, a gene encoding PglF enzyme function, a gene encoding PglE enzyme function, a gene encoding PglD enzyme function, a gene encoding LegI enzyme function, a gene encoding LegG enzyme function, a gene encoding a GlcNAc-6-P mutase, and a gene encoding a GlcNAc-1-P uridyltransferase.
 11. (canceled)
 12. The recombinant cell of claim 10, further comprising at least one of an inactivated nanT sialic acid transporter gene, an inactivated nanA sialic acid aldolase gene, an inactivated wecA undecaprenyl-P/UDP-GlcNAc transferase gene, an inactivated nanE ManNAc-6-P epimerase gene or a gene encoding an acetyl-CoA synthase.
 13. (canceled)
 14. (canceled)
 15. The recombinant cell of claim 10, wherein the recombinant cell is an E. coli cell and comprises an inactivated nanT sialic acid transporter gene, an inactivated nanA sialic acid aldolase gene, an inactivated nagA GlcNAc-6-P deacetylase gene, a PglF gene encoding SEQ ID NO:6, a PglE gene encoding SEQ ID NO:7, a PglD gene encoding SEQ ID NO:8, a LegI gene encoding SEQ ID NO:9 or SEQ ID NO:10, a LegG gene encoding SEQ ID NO:11, the agm1 GlcNAc-6-P mutase gene, and the uap1 GlcNAc-1-P uridyltransferase gene.
 16. (canceled)
 17. (canceled)
 18. The method of claim 21, wherein growth medium for the recombinant cell is supplemented with palmitate.
 19. (canceled)
 20. A method for the production of pseudaminic acid, comprising growing the recombinant cell of claim 1 and recovering the produced pseudaminic acid.
 21. A method for the production of legionaminic acid, comprising growing the recombinant cell of claim 10 and recovering the produced legionaminic acid.
 22. A recombinant cell for the production of UDP-2,4-diacetamido-2,4,6-trideoxy-β-L-altropyranose (UDP-6-deoxy-AltdiNAc), comprising an inactivated GlcNAc-6-P deacetylase gene, a gene encoding PseB enzyme function, a gene encoding PseC enzyme function, a gene encoding PseH enzyme function, a gene encoding GlcNAc-6-P mutase, and a gene encoding a GlcNAc-1-P uridyltransferase.
 23. (canceled)
 24. The recombinant cell of claim 22, further comprising at least one of an inactivated nanT sialic acid transporter gene, an inactivated nanA sialic acid aldolase gene or a gene encoding acetyl-CoA synthase.
 25. (canceled)
 26. (canceled)
 27. The recombinant cell of claim 22, wherein the recombinant cell is an E. coli cell and comprises an inactivated nanT sialic acid transporter gene, an inactivated nanA sialic acid aldolase gene, an inactivated nagA GlcNAc-6-P deacetylase gene, a PseB gene encoding SEQ ID NO:1, a PseC gene encoding SEQ ID NO:2, a PseH gene encoding SEQ ID NO:3, the agm1 GlcNAc-6-P mutase gene, and the uap1 GlcNAc-1-P uridyltransferase gene.
 28. A method for the production of UDP-2,4-diacetamido-2,4,6-trideoxy-β-L-altropyranose (UDP-6-deoxy-AltdiNAc), comprising growing the recombinant cell of claim 22 and recovering the produced UDP-6-deoxy-AltdiNAc.
 29. A recombinant cell for the production of UDP-2,4-diacetamido-2,4,6-trideoxy-α-D-glucopyranose (UDP-BacdiNAc), comprising an inactivated GlcNAc-6-P deacetylase gene, a gene encoding PglF enzyme function, a gene encoding PglE enzyme function, a gene encoding PglD enzyme function, a gene encoding GlcNAc-6-P mutase, and a gene encoding a GlcNAc-1-P uridyltransferase.
 30. (canceled)
 31. The recombinant cell of claim 29, further comprising at least one of an inactivated nanT sialic acid transporter gene, an inactivated nanA sialic acid aldolase gene, an inactivated wecA undecaprenyl-P/UDP-GlcNAc transferase gene or a gene encoding acetyl-CoA synthase.
 32. (canceled)
 33. (canceled)
 34. (canceled)
 35. (canceled)
 36. The recombinant cell of claim 29, wherein the recombinant cell is an E. coli cell and comprises an inactivated nanT sialic acid transporter gene, an inactivated nanA sialic acid aldolase gene, an inactivated nagA GlcNAc-6-P deacetylase gene, a PglF gene encoding SEQ ID NO:6, a PglE gene encoding SEQ ID NO:7, a PglD gene encoding SEQ ID NO:8, the agm1 GlcNAc-6-P mutase gene, and the uap1 GlcNAc-1-P uridyltransferase gene.
 37. The recombinant cell for the production of UDP-BacdiNAc of claim 29, wherein the cell is that of IDAC deposit No. 060411-01.
 38. A method for the production of UDP-2,4-diacetamido-2,4,6-trideoxy-α-D-glucopyranose (UDP-BacdiNAc), comprising growing the recombinant cell of claim 29 and recovering the produced UDP-BacdiNAc.
 39. The method of claim 28, wherein growth medium for the recombinant cell is supplemented with palmitate.
 40. The method of claim 38, wherein growth medium for the recombinant cell is supplemented with palmitate. 